In-situ upgrading of biomass pyrolysis vapors: Catalyst screening on a fixed bed reactor

S. D. Stefanidis*, K. G. Kalogiannis, E. F. Iliopoulou, A. A. Lappas, P. A. Pilavachi

*Corresponding author for this work

Research output: Contribution to journalArticlepeer-review

Abstract

In-situ catalytic upgrading of biomass fast pyrolysis vapors was performed in a fixed bed bench-scale reactor at 500°C, for catalyst screening purposes. The catalytic materials tested include a commercial equilibrium FCC catalyst (E-cat), various commercial ZSM-5 formulations, magnesium oxide and alumina materials with varying specific surface areas, nickel monoxide, zirconia/titania, tetragonal zirconia, titania and silica alumina. The bio-oil was characterized measuring its water content, the carbon-hydrogen-oxygen (by difference) content and the chemical composition of its organic fraction. Each catalytic material displayed different catalytic effects. High surface area alumina catalysts displayed the highest selectivity towards hydrocarbons, yielding however low organic liquid products. Zirconia/titania exhibited good selectivity towards desired compounds, yielding higher organic liquid product than the alumina catalysts. The ZSM-5 formulation with the highest surface area displayed the most balanced performance having a moderate selectivity towards hydrocarbons, reducing undesirable compounds and producing organic liquid products at acceptable yields.

Original languageEnglish
Pages (from-to)8261-8267
Number of pages7
JournalBioresource Technology
Volume102
Issue number17
DOIs
Publication statusPublished - 1 Sep 2011

Keywords

  • Bio-oil
  • Biomass
  • Catalytic upgrading
  • Deoxygenation
  • Pyrolysis

Fingerprint Dive into the research topics of 'In-situ upgrading of biomass pyrolysis vapors: Catalyst screening on a fixed bed reactor'. Together they form a unique fingerprint.

Cite this